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EP0472605B2 - Installation et procede pour traitement thermique d'effluents gazeux - Google Patents
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EP0472605B2 - Installation et procede pour traitement thermique d'effluents gazeux - Google Patents

Installation et procede pour traitement thermique d'effluents gazeux Download PDF

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Publication number
EP0472605B2
EP0472605B2 EP90908157A EP90908157A EP0472605B2 EP 0472605 B2 EP0472605 B2 EP 0472605B2 EP 90908157 A EP90908157 A EP 90908157A EP 90908157 A EP90908157 A EP 90908157A EP 0472605 B2 EP0472605 B2 EP 0472605B2
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EP
European Patent Office
Prior art keywords
heat
accumulator
regenerators
waste
gas
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
EP90908157A
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German (de)
English (en)
Other versions
EP0472605B1 (fr
EP0472605A1 (fr
Inventor
Walter Dipl.-Ing. Kanzler
Johannes Dipl.-Ing. Schedler
Heimo Dr. Thalhammer
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
DIPL.-ING. JOHANNES SCHEDLER;DR. HEIMO THALHAMMER
Original Assignee
Schedler Johannes Dipling
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Application filed by Schedler Johannes Dipling filed Critical Schedler Johannes Dipling
Publication of EP0472605A1 publication Critical patent/EP0472605A1/fr
Publication of EP0472605B1 publication Critical patent/EP0472605B1/fr
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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
    • F23G7/061—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating
    • F23G7/065—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating using gaseous or liquid fuel
    • F23G7/066—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating using gaseous or liquid fuel preheating the waste gas by the heat of the combustion, e.g. recuperation type incinerator
    • F23G7/068—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating using gaseous or liquid fuel preheating the waste gas by the heat of the combustion, e.g. recuperation type incinerator using regenerative heat recovery means
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00—Arrangements of devices for treating smoke or fumes
    • F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D17/00—Regenerative heat-exchange apparatus in which a stationary intermediate heat-transfer medium or body is contacted successively by each heat-exchange medium, e.g. using granular particles
    • F28D17/02—Regenerative heat-exchange apparatus in which a stationary intermediate heat-transfer medium or body is contacted successively by each heat-exchange medium, e.g. using granular particles using rigid bodies, e.g. of porous material
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P80/00—Climate change mitigation technologies for sector-wide applications
    • Y02P80/10—Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
    • Y02P80/15—On-site combined power, heat or cool generation or distribution, e.g. combined heat and power [CHP] supply

Definitions

  • the invention relates to a plant and a method for the thermal oxidation of organic kollen material compounds.
  • recuperators Shell and tube heat exchanger or plate heat exchanger
  • regenerators designed as regenerators
  • Regenerators were already used as hot air heaters used for blast furnaces a long time ago also recently in the exhaust gas cleaning success used.
  • the individual regenerators are with various Fills filled, which have the disadvantage that they only allow low flow speeds, if the pressure drops are kept low should.
  • one of the channels is in the regenerators crossed, made of chamotte stones Latticework provided as a heat storage mass.
  • Latticework provided as a heat storage mass.
  • the pressure loss relatively low, and they allow a higher flow rate the one to be thermally treated Gases, due to the relatively large free cross sections for the flow and the relatively high cross sections however, the stone itself is the heat exchange delayed, so that efficiencies in the range of maximum about 90% can be reached.
  • the invention has for its object a Plant and a process to create the the disadvantages of the previously known systems and method avoids and with minimal abrasion in the case of dust-like particles in the exhaust gas, with high Space and dimensional stability, furthermore with simple Structure and easy manipulation of the individual elements the heat accumulator has high throughput speeds with low pressure drops and thus compact sizes and high efficiency allowed during heat exchange itself. It was found that heat storage masses with defined, honeycomb bodies arranged in spatial order are built up for alternate heating and cooling of flowing gases in particular are effective.
  • the invention thus relates to a system and a method for the thermal oxidation of organic carbon compounds according to claim 1 or 6.
  • honeycomb bodies without catalytic action as a gas flow rectifier, especially in exhaust and Flue gas treatment plants.
  • the invention exists in a completely new way now in it, with those known per se in their basic form Honeycomb bodies extremely effective heat storage to build up and thus regenerator plants equip for the purpose mentioned at the beginning.
  • Special advantage of using the prism body their heat storage is completely unproblematic Installation in the regenerator towers, whereby a high mechanical stability of the structure as a result the regular shape of the individual elements becomes.
  • the ratio between freely flowable Cross section and that taken up by the storage body itself Volume is for a high direction of heat transfer the pressure losses are particularly advantageous are easy to keep to a minimum.
  • Another advantage of the new system is its low energy consumption, since autothermal operation is already achieved with pollutant levels above 0.5 - 1 g / Nm 3 .
  • the regenerator stores over 97% of the heat required for combustion, less than 3% remain in the clean gas. Therefore, with pollutant contents of over 2 g / Nm 3, the production of excess energy in the form of process steam or hot water can already be economical.
  • the calorific value of concentration peaks can be stored in the regenerator and used evenly, liquid waste can be used as an additional fuel. Heating can be carried out using natural gas, liquid gas, sulfur-free liquid fuels or electricity, the latter only if the pollutant content is above 1 g / Nm 3 .
  • the storage mass is obtained by extrusion of corresponding ceramic masses for each required temperatures are produced, preferably made of earthenware, porcelain, mullite or other masses which are known to the person skilled in the art.
  • the specific surface of the storage mass is important of the new regenerators within the above range.
  • the flow velocity in the individual storage bodies is chosen between 2 and 10 m / s, so that the pressure losses do not become too high.
  • good heat transfer can be achieved, so that efficiencies for heat recovery of around 97-98% can be achieved, which means that at a raw gas temperature of 100 ° C and a combustion temperature of 800 ° C, the exhaust gas only 21 ° C must be heated, or that the exhaust gas burns without the supply of additional fuel if only 1 / Nm 3 of pollutant with a heat of combustion of about 6000 kcal / kg is contained in the exhaust gas
  • the heat storage masses of the regenerators forming a Layer or "layer”, with a plurality of with at least a part of their prism surfaces adjacent to each other arranged storage bodies formed are particularly high mechanical stability the one made up of the single prism bodies Storage masses practically without “gas and heat exchange slip" guaranteed between the storage bodies.
  • the heat storage masses of the regenerators with at least two in the direction of the respective gas flow at a distance from each other, with their prism surfaces, especially with their channels, aligned aligned storage bodies formed are.
  • the heat storage masses of the regenerators with at least two in the direction of the respective gas flow at a distance from each other, with their prism surfaces, especially with their channels, aligned aligned storage bodies formed are.
  • the quotient is below the hydraulic diameter from four times the cross-sectional area of the channel to understand by its scope.
  • the heat storage masses of the regenerators are formed with storage bodies, the channels of which each have a cross-sectional area of 3 to 25 mm 2 through which gas can flow.
  • the invention enables, with approximately the same investment costs per m 2 of exchange area as in the case of storage masses customary to date, formed with packing elements, and with a long service life, a high efficiency in heat recovery in the range of at least 97%.
  • the invention is closer 1 shows schematically an inventive Storage body in oblique view, 2 shows a view of a prism end face for the system provided storage body according to the invention with examples of different channel cross sections and,
  • Figure 3 is a schematic representation of a Plant for thermal exhaust gas or exhaust air oxidation is provided according to the invention.
  • FIG.1 here square-prismatic Storage body 10 with prism outer surface 13 with edges of length k and the two prism end faces 11 and 12 with boundary sides s points in the gas flow direction r1 or r2 and extending parallel to the main prism axis a Channels 15 square cross-section on.
  • a plurality of such similar storage bodies 10 can with their prism surfaces 13 adjacent to each other Form layers of storage bodies, which cursing, in Plurality one above the other - at a distance from each other - Are arranged in a regenerator whereby finally a storage mass each desired Total volume is built up.
  • the material the storage body 10 is advantageously a thermostable oxide ceramic Material with preferably "dense" shards.
  • FIG. 2 shows the geometry of the invention honeycomb provided for heat transfer square-prismatic storage body 10 based on a view in front of them Prism end face 11.
  • the body points at rounded Main prism edges, preferably 0.5 m Length and prism end sides with preferably about 0.15 m in length a large number of regularly arranged continuous channels 15 with square Cross-sectional area, being for demonstration purposes four areas I - IV with channels different Dimensions, namely with 10, 8, 5 and 2 mm side length b, are shown, the region I not according to the invention.
  • Channels of dimension and arrangement according to areas III and IV are particularly preferred, because high efficiencies in the removal of pollutants ensure even the smallest concentrations in exhaust air or exhaust gases, the geometric surface area of the latter being approximately 800 m 2 / m 3 of storage body mass.
  • the width of the webs 16 is 0.5 to 1 mm.
  • the regenerator parts consist of three storage masses formed with storage bodies provided according to the invention, one of which is alternately in the cooling phase, one in the heating phase and one in the rinsing phase.
  • the cooling phase the cold raw gas with the hot storage mass is heated from 60 ° C to 750 ° C, in the combustion chamber the gas flow is increased by the heat of combustion of the acetone from 750 to 775 ° C and by heating from 775 ° C to 780 ° C heated.
  • the 780 ° C hot gas stream then reaches the regenerator part which is in the heating phase and is cooled there to 90 ° C.
  • the third regenerator part is flushed with approx. 5 - 10% of the clean gas flow during this time, so that no untreated exhaust air gets into the clean gas when the gas flow is switched over.
  • the storage masses are all the same and each consist of eight elements with a cross section of 150 x 150 mm and six elements with a length of 300 mm, each oriented in the direction of flow.
  • the geometry of the individual elements is carried out according to FIGS. 1 and 2, the spacing of the webs from one another is 3 mm and the web thickness is 1 mm, which results in the geometric surface of the elements with 800 m 2 / m 3 .
  • the regenerators are switched every 3 minutes and the pressure drop per regenerator is 20 mbar.
  • Acetone could be found in the purified exhaust gas can no longer be proven.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Incineration Of Waste (AREA)
  • Exhaust Gas After Treatment (AREA)
  • Air Supply (AREA)

Claims (7)

  1. Installation destinée à l'oxydation thermique de composés organiques de carbone, en particulier d'hydrocarbures, dans des flux de gaz y compris d'air d'échappement, éventuellement pour l'épuration de gaz, avec récupération régénératrice de chaleur, le flux de gaz d'échappement étant en alternance réchauffé et refroidi dans au moins deux régénérateurs (1010, 1020, 1030) présentant chacun des masses d'accumulation de chaleur (101, 102, 103) céramiques, caractérisée en ce que la masse d'accumulation de chaleur (101, 102, 103) respective des régénérateurs (1010, 1020, 1030) est constituée avec des corps accumulateurs (10) sensiblement en forme de prismes, agencés avec l'axe principal du prisme (a) sensiblement dans le sens d'écoulement de gaz (r1, r2), dont l'intérieur respectif présente une multitude de canaux (15) traversants, qui débouchent dans les deux faces d'extrémité (11, 12) du prisme et s'étendent sensiblement parallèles à l'axe principal (a) du prisme et sensiblement rectilignes avec des sections de canaux sensiblement identiques, les masses d'accumulation de chaleur (101, 102, 103) des régénérateurs étant constituées avec des corps accumulateurs de chaleur (10) avec une surface spécifique entre 200 et 1000 m2/m3, dont les canaux (15) présentent un diamètre hydraulique de 2 mm à 8 mm et chacun une superficie en section autorisant le passage du gaz de 3 à 25 mm2, et dont les nervures (16) présentent entre les canaux (15) une largeur de 0,5 mm à 1 mm, la longueur (k) du prisme des corps accumulateurs étant de 0,2 m à 0,6 m et dont la longueur latérale de surfaces d'extrémité de prisme (s) est de 0,1 m à 0,5 m, les masses d'accumulation de chaleur (101, 102, 103) étant réalisées par extrusion de masses céramiques et les masses d'accumulation de chaleur (101, 102, 103) étant constituées en formant au moins deux couches agencées à distance l'une de l'autre avec chacune une multitude de corps accumulateurs de chaleur (10) disposés les uns à côté des autres avec leurs surfaces enveloppes (13) du prisme, deux corps accumulateurs (10) disposés l'un derrière l'autre en direction du flux de gaz respectif (r1, r2) étant disposés en alignement à distance l'un de l'autre avec leurs surfaces (13) de prisme, en particulier avec leurs canaux (15).
  2. Installation selon la revendication 1, caractérisée en ce que les masses d'accumulation de chaleur (101, 102, 103) des régénérateurs (1010, 1020, 1030) sont constitués avec des corps accumulateurs (10) dont les canaux (15) présentent des sections de géométrie similaire à la section de prisme des corps accumulateurs (10).
  3. Installation selon la revendication 1 ou 2, caractérisée en ce que les masses d'accumulation de chaleur (101, 102, 103) des régénérateurs (1010, 1020, 1030) sont constituées avec des corps accumulateurs (10) qui présentent entre eux les mêmes sections de prisme, de préférence rectangulaires, carrées ou régulièrement hexagonales.
  4. Installation selon l'une des revendications 1 à 3, caractérisé en ce que les masses d'accumulation de chaleur (101, 102, 103) des régénérateurs (1010, 1020, 1030) sont constituées avec des corps accumulateurs (10) dont les canaux (15) présentent chacun une superficie de section, autorisant le passage de gaz, d'au moins 4 mm2.
  5. Installation selon l'une des revendications 1 à 4, caractérisé en ce que les masses d'accumulation de chaleur (101, 102, 103) des régénérateurs (1010, 1020, 1030) sont constituées avec des corps accumulateurs (10) avec une masse de porcelaine ou de mullite cuite entre 1300°C et 1600°C.
  6. Procédé d'oxydation thermique de composés organiques de carbone, en particulier d'hydrocarbures dans des flux de gaz d'échappement avec récupération régénératrice de chaleur, le flux de gaz d'échappement étant en alternance réchauffé et de nouveau refroidi dans au moins deux régénérateurs (1010, 1020, 1030), le flux de gaz d'échappement réchauffé dans la masse d'accumulation de chaleur échauffée continuant d'être chauffé dans une chambre de combustion (4) par la chaleur de combustion des composés d'hydrocarbures organiques et étant chauffé ultérieurement avec un chauffage (6), et le flux de gaz d'échappement étant aspiré au moyen d'une soufflante (5) par les régénérateurs (101, 1020, 1030), caractérisé en ce que le flux de gaz d'échappement est guidé à travers une des masses d'accumulation de chaleur (101, 102, 103) indiquées dans l'une des revendications 1 à 5.
  7. Utilisation des corps accumulateurs de chaleur (10) sensiblement en forme de prismes, agencés avec l'axe principal de prisme (a) sensiblement dans le sens d'écoulement de gaz (r1, r2), du type indiqué dans la revendication 1, pour former des masses d'accumulation de chaleur (101, 102, 103) de régénérateurs dans des installations ou des procédés d'oxydation thermique de composés de carbone organiques, en particulier d'hydrocarbures, dans des flux de gaz d'échappement avec récupération de chaleur régénératrice, le flux de gaz d'échappement étant en alternance réchauffé et de nouveau refroidi dans au moins deux régénérateurs (1010, 1020, 1030) présentant chacun les masses d'accumulation de chaleur (101, 102, 103), le flux de gaz d'échappement réchauffé dans la masse d'accumulation de chaleur échauffée continuant d'être chauffé dans une chambre de combustion (4) par la chaleur de combustion des composés d'hydrocarbures organiques et étant chauffé ultérieurement avec un chauffage (6), et le flux de gaz d'échappement étant aspiré au moyen d'une souffleuse (5) par les régénérateurs.
EP90908157A 1989-05-17 1990-05-17 Installation et procede pour traitement thermique d'effluents gazeux Expired - Lifetime EP0472605B2 (fr)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
AT116889 1989-05-17
AT0116889A ATA116889A (de) 1989-05-17 1989-05-17 Verfahren zur thermischen abgasverbrennung
AT1168/89 1989-05-17
PCT/AT1990/000047 WO1990014560A1 (fr) 1989-05-17 1990-05-17 Installation et procede pour traitement thermique d'effluents gazeux

Publications (3)

Publication Number Publication Date
EP0472605A1 EP0472605A1 (fr) 1992-03-04
EP0472605B1 EP0472605B1 (fr) 1993-12-08
EP0472605B2 true EP0472605B2 (fr) 2003-01-22

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EP90908157A Expired - Lifetime EP0472605B2 (fr) 1989-05-17 1990-05-17 Installation et procede pour traitement thermique d'effluents gazeux

Country Status (4)

Country Link
EP (1) EP0472605B2 (fr)
AT (2) ATA116889A (fr)
DE (1) DE59003808D1 (fr)
WO (1) WO1990014560A1 (fr)

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DE102009055942A1 (de) 2009-11-26 2011-06-01 Chemisch-Thermische Prozesstechnik Gmbh Verfahren und Vorrichtung zur Reinigung von Abgasen
DE102017101507A1 (de) 2017-01-26 2018-07-26 Chemisch Thermische Prozesstechnik Gmbh Verfahren und Vorrichtung zur Abgasreinigung
US20230279333A1 (en) * 2015-06-10 2023-09-07 Brisa International, Llc System and method for biomass growth and processing

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HUT69307A (en) * 1993-06-15 1995-09-28 Grace W R & Co Method for coating heat transfer packing material with catalyst and/or adsorbent and process for use of packings in regenerative incineration systems
US5707229A (en) * 1993-07-12 1998-01-13 Durr Industries, Inc. Regenerative thermal oxidizer with heat exchanger columns
US5658541A (en) * 1995-03-16 1997-08-19 Monsato Company Process for removal of divalent sulfur compounds from waste gases
AT402697B (de) * 1995-08-17 1997-07-25 Schedler Johannes Verfahren zur thermischen abreinigung von regenerativen nachverbrennungsanlage ohne schastoffreisetzung und ohne unterbrechung des hauptgasstrommes
US5919425A (en) * 1995-09-21 1999-07-06 Engelhard Corporation Catalyzed packing material for regenerative catalytic oxidation
US5770162A (en) * 1996-07-08 1998-06-23 Norton Chemical Process Products Corporation Horizontal regenerative thermal oxidizer unit
US5753197A (en) * 1996-11-01 1998-05-19 Engelhard Corporation Method of purifying emissions
DE19747905C1 (de) * 1997-10-30 1999-01-28 Chemisch Thermische Prozestech Vorrichtung zur Reinigung von schadstoffhaltigem Abgas
US6322356B1 (en) 2000-09-28 2001-11-27 Durr Environmental, Inc. Pollution abatement reactor system having nonprismatic structured media
DE10214567C1 (de) * 2002-04-02 2003-09-04 Johannes Schedler Verfahren und Vorrichtung zur Beseitigung von Ammoniak aus Abgasen
DE10229405B4 (de) * 2002-06-29 2006-01-26 Eisenmann Maschinenbau Gmbh & Co. Kg Keramischer Wabenkörper zur Verwendung in einer thermischen Abgasbehandlungsvorrichtung
DE10234771B4 (de) * 2002-07-30 2004-08-26 Rauschert Verfahrenstechnik Gmbh Wärmespeicherbett für regenerative Wärmeübertragung
AT6318U1 (de) * 2002-10-22 2003-08-25 Johann Dipl Ing Roitner Formkörper und verwendung eines formkörpers
DE102004022737B4 (de) * 2004-05-07 2006-01-12 Johannes Dipl.-Ing. Schedler Verfahren und Vorrichtung zur Reinigung von aerosol- und staubbelasteten Abgasströmen
DE102007032952B4 (de) * 2006-09-12 2010-07-08 Kba-Metalprint Gmbh Verfahren zum Betreiben einer thermisch-regenerativen Abluftreinigungsanlage
DE102006058696B4 (de) * 2006-12-13 2008-12-18 Eisenmann Anlagenbau Gmbh & Co. Kg Vorrichtung zur regenerativen Nachverbrennung von klebrigen Schadstoffpartikeln in Abgas und Verfahren zum Betreiben einer solchen
DE102008011938B3 (de) * 2008-02-29 2009-09-10 Arge Schedler - Thalhammer Vorrichtung zur Reinigung von schadstoffhaltigem Abgas
EP2105663B1 (fr) 2008-03-28 2016-01-06 Cesare Baldassari Dispositif d'exécution de processus thermiques, dans lesquels une flamme est utilisée comme source d'énergie thermique
DE102008055852A1 (de) 2008-11-04 2010-05-06 Kba-Metalprint Gmbh Vorrichtung zum Wärmeübertragen sowie Abgasreinigungseinrichtung und Verfahren zum Übertragen von Wärme
DE102009009579B4 (de) 2009-02-19 2015-01-08 Chemisch-Thermische Prozesstechnik Gmbh Verfahren zum Beschichten der Kanäle eines Wabenkörpers, Vorrichtung zur Durchführung des Verfahrens und Verwendung des beschichteten Wabenkörpers
DE102009023600B4 (de) 2009-06-02 2011-05-12 Ctp Chemisch Thermische Prozesstechnik Gmbh Verfahren und Vorrichtung zur Reinigung von Abgasströmen
DE102010048040B4 (de) 2010-10-12 2017-02-23 Ctp Chemisch Thermische Prozesstechnik Gmbh Verfahren und Vorrichtung zur Reinigung lachgashaltiger Abgase
DE102010048308B4 (de) 2010-10-14 2016-06-16 Ctp Chemisch Thermische Prozesstechnik Gmbh Vorrichtung zur Reinigung von schadstoffhaltigem Abgas
CN102563670A (zh) * 2010-12-21 2012-07-11 热能加工技术化学有限公司 用于净化污染废气的设备和方法
AT513563B1 (de) 2012-11-08 2014-09-15 Ibiden Porzellanfabrik Frauenthal Gmbh Wabenkörper aus Keramikmaterial
DE202013100418U1 (de) 2013-01-29 2013-04-16 Chemisch Thermische Prozesstechnik Gmbh Vorrichtung zur Reinigung von Abgasen
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DE102013109977A1 (de) * 2013-09-11 2015-03-12 Thyssenkrupp Industrial Solutions Ag Verfahren und Anlage zur Reinigung von Abgasen mit einer regenerativen Nachverbrennungsanlage
DE102014013181A1 (de) * 2014-09-05 2016-03-10 Torsten Sahrhage Verfahren und Vorrichtung zur Abgasreinigung
DE102015108014B3 (de) 2015-05-20 2016-11-24 Chemisch Thermische Prozesstechnik Gmbh Verfahren und Anlage zur Reinigung von mit Stickoxiden beladenen Abgasen
DE102016102506A1 (de) * 2015-12-22 2017-06-22 Elringklinger Ag Packung und Kolonne umfassend eine oder mehrere Packungen
DE102017008634B4 (de) * 2017-09-14 2025-10-02 Vdeh-Betriebsforschungsinstitut Gmbh Vorrichtung zur Wärmerückgewinnung, eine Verwendung eines Speicherkörpers in einer Vorrichtung zur Wärmerückgewinnung sowie ein Verfahren zur Wärmerückgewinnung
EP4684866A1 (fr) 2024-07-26 2026-01-28 Scheuch Management Holding GmbH Procédé pour la purification de gaz de fumée contenant des matières organiques gazeuses

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DE102009055942A1 (de) 2009-11-26 2011-06-01 Chemisch-Thermische Prozesstechnik Gmbh Verfahren und Vorrichtung zur Reinigung von Abgasen
US20230279333A1 (en) * 2015-06-10 2023-09-07 Brisa International, Llc System and method for biomass growth and processing
US12600937B2 (en) * 2015-06-10 2026-04-14 Brisa International, Llc System and method for biomass growth and processing
DE102017101507A1 (de) 2017-01-26 2018-07-26 Chemisch Thermische Prozesstechnik Gmbh Verfahren und Vorrichtung zur Abgasreinigung
FR3062071A1 (fr) 2017-01-26 2018-07-27 Chemisch Thermische Prozesstechnik Gmbh Procede et dispositif pour l'epuration d'effluents gazeux
DE102017101507B4 (de) 2017-01-26 2022-10-13 Chemisch Thermische Prozesstechnik Gmbh Verfahren und Vorrichtung zur Abgasreinigung

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EP0472605B1 (fr) 1993-12-08
DE59003808D1 (de) 1994-01-20
EP0472605A1 (fr) 1992-03-04
ATA116889A (de) 1997-11-15
WO1990014560A1 (fr) 1990-11-29

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